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Multifunctional continuous phase transition extraction device

An extraction device and multi-functional technology, which is applied in the new device field of multi-functional continuous phase change extraction technology in extraction and separation, can solve the problems of equipment volume enlargement, limitation, low extraction temperature and pressure, etc., and achieves high efficiency and full function. Effect

Active Publication Date: 2014-09-03
曹庸
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Solvent extraction method is widely used because of its low cost, simple equipment, and wide application range, but there are problems such as low extraction efficiency, inconvenient filtration after extraction, and inconvenient solvent recovery.
Reflux extraction, such as the Chinese patent with the publication number CN1454694A discloses a heat reflux high-pressure extraction-vacuum concentration process, which can extract, filter, and concentrate at the same time, but what the extraction device uses is a spray design, and the pressure is the highest. It can reach 0.1MPa, the solvent used is limited, and the efficiency has not been greatly improved
Supercritical extraction technology, such as the Chinese patent with publication number CN201799133U discloses a supercritical CO 2 Fluid extraction device, this technology is environmentally friendly, the solvent is cheap and easy to get, and the substances can be separated better, but it also has very big disadvantages: 1. It only has a good extraction effect on non-polar substances, but it has a good extraction effect on polar substances. The extraction effect is poor; two, the extraction must be carried out under an ultra-high pressure state above 20MPa, and the extremely high pressure limits the enlargement of the equipment volume; three, its equipment manufacturing cost and maintenance cost are too high, these factors have limited this The development of technology, so it is not widely used
Subcritical extraction technology, such as the Chinese patent with publication number CN101642632A discloses a subcritical fluid extraction device and method for active ingredients of natural products. subcritical extraction medium, but there is a long extraction time and a large demand for extraction solvents, which cannot get rid of the problem of intermittent operation of conventional solvent extraction
The Chinese patent with publication number CN102258882A discloses "a device for dynamic extraction using subcritical fluid" based on the original basis of the Chinese patent with publication number CN101642632A "subcritical fluid extraction device and method for active ingredients of natural products" Improvements have been made to change the problem of the batch operation of conventional solvent extraction, but it also has a better extraction effect on non-polar substances, and poor extraction effects on polar substances.

Method used

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  • Multifunctional continuous phase transition extraction device

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] (1) Camellia oil fruit (crushed to 20 mesh, dried to make the moisture ≤ 5%) weighed 7KG, put it directly into the extraction tank 1, pressurized by the high-pressure pump 7 to make n-butane pass through the heat exchanger 8I, and enter Extraction in the extraction tank 1, the extraction temperature is 45°C, and the extraction pressure is 0.5MPa; the solvent passing through the extraction tank 1 enters the analysis tank 2I with oil, and is analyzed in the analysis tank 2I, the temperature of the analysis tank 2I is 55 °C, and the pressure 0.25MPa; the whole extraction time is 50min, and 1.94KG product is obtained in the first bottom valve V31 of the analysis tank 2I, and the extraction rate is verified to be 99.3%.

[0031] (2) After the oil is extracted, switch to the passage extraction tank 1, heat exchanger 8II, second pressure control valve V22, second analysis tank 2II, second purification column 3II, second condenser 4II, and second solvent tank 5II , the second v...

Embodiment 2

[0033] (1) Weigh 10KG of castor beans, press hydraulic pressure first, squeeze out 3KG of oil, then crush the meal to 20 mesh, dry to make the moisture ≤ 5%, put it directly into the extraction tank 1, and pressurize it by the high-pressure pump 7 Make n-butane pass through the first heat exchanger 8I, and then enter the extraction tank 1 for extraction, the extraction temperature is 80°C, and the extraction pressure is 1.0MPa; the solvent passing through the extraction tank 1 enters the first analysis tank 2I with oil , analyzed in the first analysis tank 2I, the analysis temperature is 60°C, the pressure is 0.3MPa, the whole extraction time is 150min, and 1.97KG product is obtained in the first bottom valve V31 of the first analysis tank 2I, and the verified extraction rate is 98.5 %.

[0034] (2) After the oil is extracted, switch to the passage extraction tank 1, the second heat exchanger 8II, the second pressure control valve V22, the second desorption tank 2II, the secon...

Embodiment 3

[0036] (1) Weigh 7KG of soybeans fermented with soy sauce (crushed to 40 mesh, dried to make the moisture ≤ 10%), put them directly into the extraction tank 1, pressurize the high-pressure pump 7 to make the propane pass through the heat exchanger 8I, and enter Extract in the extraction tank 1, the extraction temperature is 45°C, and the extraction pressure is 1.2MPa; the solvent passing through the extraction tank 1 enters the first analysis tank 2I with oil, and is analyzed in the first analysis tank 2I, and the analysis temperature is 60 ℃, the pressure is 0.35MPa, the whole extraction time is 65min, and 2.02KG product is obtained in the first bottom valve V31 of the first desorption tank 2I, and the extraction rate is verified to be 99%.

[0037] (2) After the oil is extracted, switch to the passage extraction tank 1, the second heat exchanger 8II, the second pressure control valve V22, the second desorption tank 2II, the second purification column 3II, the second condenser...

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Abstract

A multifunctional continuous phase transition extraction device comprises an extraction system, an analysis system and a solvent reclaiming system, wherein the extraction system comprises a first heat exchanger (8I), a extraction tank (1); the analysis system comprises a second heat exchanger (8II) and a first analysis tank (2I), a second analysis tank (2II), a first purifying pillar (3I), and a second purifying pillar (3II); the solvent reclaiming system comprises a first condenser (4I), a second condenser (4II), a first solvent tank (5I), and a second solvent tank (5II). According to the device, two paths of extraction circuits are formed. During the whole extraction process, the phase transition process of an extracting agent is instant and continuous; the extracting agent can be subjected to continuous phase transition and can be recycled, so that target objects can be extracted to the utmost extent, and accordingly, the efficiency is very high and the solvent consumption is small. Moreover, the whole process is performed in a sealed and low-pressure environment, the function is complete, and the purposes of safety and reliability are achieved. Therefore, the device is suitable for extraction of most natural products.

Description

technical field [0001] The invention relates to the technical field of extraction and separation, and is a new device for extraction and separation of multifunctional continuous phase change extraction technology. Background technique [0002] At present, the methods commonly used in the extraction of natural products include solvent extraction, reflux extraction, supercritical carbon dioxide extraction, subcritical extraction, etc. Solvent extraction method is widely used because of its low cost, simple equipment and wide application range, but there are problems such as low extraction efficiency, inconvenient filtration after extraction, and inconvenient solvent recovery. Reflux extraction, such as the Chinese patent with the publication number CN1454694A discloses a heat reflux high-pressure extraction-vacuum concentration process, which can extract, filter, and concentrate at the same time, but what the extraction device uses is a spray design, and the pressure is th...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D11/02C11B1/10
Inventor 曹庸刘汉槎戴伟杰张泳管晓盛
Owner 曹庸
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